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    • 55. 发明授权
    • Method and apparatus for anaerobic digestion of organic liquid waste streams
    • 有机废液流厌氧消化的方法和装置
    • US08470177B2
    • 2013-06-25
    • US12516104
    • 2006-11-27
    • Stephen W. Dvorak
    • Stephen W. Dvorak
    • C02F3/28C02F11/04
    • C12M21/04C02F3/286C02F3/34C02F11/04C02F2209/02C02F2209/06C12M23/34C12M27/20C12M41/24C12M41/26Y02E50/343Y02W10/23
    • A system and method for treating high-strength organic liquid waste. Generally, the method includes feeding influent high-strength organic liquid waste including organic molecules to an anaerobic digester, converting at least a portion of the organic molecules in the liquid waste to acids using acid forming bacteria, converting at least a portion of the acids in the liquid waste to methane using methanogenic bacteria, separating the liquid waste after treatment with the methanogenic bacteria into alkaline sludge and effluent, and using the alkaline sludge to adjust the pH of the liquid waste in the anaerobic digester. In the case of acidic high-strength organic liquid wastes, a portion of the acids produced by the acid forming bacteria may be recirculated to the front of the anaerobic digester and combined with influent high-strength organic liquid waste.
    • 一种高强度有机废液处理系统及方法。 通常,该方法包括将含有有机分子的流入的高强度有机液体废物进料到厌氧消化器中,使用酸形成细菌将至少一部分液体废物中的有机分子转化成酸,将至少一部分酸转化为 使用甲烷生成细菌将液体废物排放到甲烷中,将产甲烷菌处理后的废液与碱性污泥和流出物分离,并使用碱性污泥调节厌氧消化器中废液的pH值。 在酸性高强度有机液体废物的情况下,由酸形成细菌产生的酸的一部分可以再循环到厌氧消化器的前面并与流入的高强度有机废液混合。
    • 58. 发明授权
    • Systems and methods for anaerobic digestion of biomaterials
    • 厌氧消化生物材料的系统和方法
    • US08414770B2
    • 2013-04-09
    • US13360668
    • 2012-01-28
    • Charles Satish Smith
    • Charles Satish Smith
    • C02F3/28
    • C02F3/006C02F1/683C02F3/28C02F3/34C02F3/343C02F11/04C02F11/185C02F2101/20C02F2103/20C02F2103/26C02F2209/02C02F2209/03C02F2209/04C02F2209/06C02F2209/40C02F2303/10Y02E50/343Y02W10/30
    • Systems and methods for performing anaerobic digestion of biomaterials using a clarifier, a batch reactor, and/or a digester are disclosed. The clarifier performs pretreatment processing of biomaterial to improve anaerobic digestion. The batch reactor and/or the digester are coupled to the clarifier and are configured to digest the processed biomaterial. A control system for an anaerobic digestion process includes a flow control system, a temperature control system, and a totalization system. The flow control system controls the flow of biomaterial and the delivery of chemical agents to the biomaterial based on conductivity, temperature, pressure, and/or composition of the biomaterial. The temperature control system includes a heat source and heat exchangers that control the temperature of the biomaterial. The totalization system senses the volume of biomaterial in at least one stage of an anaerobic digestion process and a controller controls the flow control system based upon the sensed volume of biomaterial.
    • 公开了使用澄清器,间歇反应器和/或蒸煮器进行生物材料厌氧消化的系统和方法。 净化器进行生物材料的预处理,以改善厌氧消化。 间歇反应器和/或蒸煮器耦合到澄清器并且被配置为消化经处理的生物材料。 用于厌氧消化过程的控制系统包括流量控制系统,温度控制系统和累计系统。 流量控制系统基于生物材料的电导率,温度,压力和/或组成来控制生物材料的流动和向生物材料递送化学试剂。 温度控制系统包括热源和控制生物材料的温度的热交换器。 累积系统在厌氧消化过程的至少一个阶段中感测生物材料的体积,并且控制器基于感测到的生物材料体积来控制流量控制系统。
    • 60. 发明申请
    • POLYHYDROXYALKANOATE PRODUCTION DURING WASTEWATER TREATMENT
    • 废水处理过程中的聚羟基烷基酯生产
    • US20130040351A1
    • 2013-02-14
    • US13206327
    • 2011-08-09
    • HSIN-YING LIUMICHAEL WAYNE FALK, JR.
    • HSIN-YING LIUMICHAEL WAYNE FALK, JR.
    • C12P7/40
    • C02F3/12C02F3/1221C02F3/1263C02F3/34C02F2209/001C02F2209/10C12P7/42C12P7/625Y02W10/15Y02W10/45
    • A wastewater treatment process elicits microorganisms to convert a waste stream/organic resource to intracellular biopolymer polyhydroxyalkanoate (PHA). The process includes (i) waste stream/organic resource composition feed criteria, (ii) configuration coupled with operational parameters, and (iii) PHA-laden biomass separation and stabilization. A waste stream/organic resource capable of producing enhanced levels of PHA may be selected based on a combination of criteria, which may include short chain fatty acid concentration, protein concentration, polysaccharides concentration, and total suspended solids concentration. The waste stream is introduced into an aeration basin upon a specific configuration and operated under various parameter combinations for selecting/enriching microorganisms capable of producing PHA. The PHA-laden biomass is separated and stabilized for downstream PHA related product beneficial uses. The present process achieves concurrent wastewater treatment and PHA production, where PHA level (of more than 10% on a cell-weight basis) otherwise could not be obtained.
    • 废水处理过程引起微生物将废物流/有机物质转化为细胞内生物聚合物聚羟基链烷酸酯(PHA)。 该过程包括(i)废物流/有机资源组合物进料标准,(ii)配置与操作参数,以及(iii)含PHA的生物质分离和稳定化。 可以基于标准的组合来选择能够产生增强的PHA水平的废物流/有机资源,其可以包括短链脂肪酸浓度,蛋白质浓度,多糖浓度和总悬浮固体浓度。 废物流根据特定的构型被引入曝气池并在各种参数组合下操作,用于选择/富集能够生产PHA的微生物。 PHA负载生物质被分离并稳定下游PHA相关产品的有益用途。 本方法实现了同时进行的废水处理和PHA生产,其中PHA水平(以细胞重量计超过10%)不能获得。